EP2289977A1 - Formules d'agents anti-moussants - Google Patents

Formules d'agents anti-moussants Download PDF

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Publication number
EP2289977A1
EP2289977A1 EP10169956A EP10169956A EP2289977A1 EP 2289977 A1 EP2289977 A1 EP 2289977A1 EP 10169956 A EP10169956 A EP 10169956A EP 10169956 A EP10169956 A EP 10169956A EP 2289977 A1 EP2289977 A1 EP 2289977A1
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EP
European Patent Office
Prior art keywords
polyethers
bonded hydrogen
organopolysiloxanes
weight
silicone
Prior art date
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EP10169956A
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German (de)
English (en)
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EP2289977B1 (fr
Inventor
Christian Dr. Herzig
Willibald Dr. Burger
Martina Joachimbauer
Josef Wimmer
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Wacker Chemie AG
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Wacker Chemie AG
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/42—Block-or graft-polymers containing polysiloxane sequences
    • C08G77/46—Block-or graft-polymers containing polysiloxane sequences containing polyether sequences
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/02—Foam dispersion or prevention
    • B01D19/04—Foam dispersion or prevention by addition of chemical substances
    • B01D19/0404—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance
    • B01D19/0409—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance compounds containing Si-atoms
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L83/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
    • C08L83/04—Polysiloxanes
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16—Organic compounds
    • C11D3/37—Polymers
    • C11D3/3703—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C11D3/373—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicones
    • C11D3/3738—Alkoxylated silicones
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C3/00—Pulping cellulose-containing materials
    • D21C3/22—Other features of pulping processes
    • D21C3/28—Prevention of foam
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/06—Paper forming aids
    • D21H21/12—Defoamers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04—Polysiloxanes
    • C08G77/12—Polysiloxanes containing silicon bound to hydrogen
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/34—Silicon-containing compounds
    • C08K3/36—Silica
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00—Use of pretreated ingredients
    • C08K9/04—Ingredients treated with organic substances
    • C08K9/06—Ingredients treated with organic substances with silicon-containing compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L83/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
    • C08L83/10—Block- or graft-copolymers containing polysiloxane sequences
    • C08L83/12—Block- or graft-copolymers containing polysiloxane sequences containing polyether sequences

Definitions

  • the ratio of the weight concentration of Si-bonded hydrogen in organopolysiloxane (1) to the weight concentration of Si-bonded hydrogen in organopolysiloxane (2) is preferably not more than 20, preferably not more than 10.
  • organopolysiloxanes (1) and (2) are used in total preferably in amounts of from 0.5 to 1.0, preferably from 0.6 to 0.8, gram atom of Si-bonded hydrogen per mole of aliphatic double bond in the polyethers (3) ,
  • a preferred procedure is the preparation of the silicone polyethers in one process step.
  • formula (III) should be understood to mean that o units - (SiR 2 O) - and p units - (SiRHO) - in in any way, for example as a block or randomly, may be distributed in the organopolysiloxane molecule.
  • organopolysiloxanes (1) are, in particular, copolymers of trimethylsiloxane, dimethylsiloxane and methylhydrogensiloxane units, copolymers of dimethylhydrogensiloxane, methylhydrogensiloxane, dimethylsiloxane and trimethylsiloxane units, copolymers of trimethylsiloxane, dimethylhydrogensiloxane and methylhydrogensiloxane units, copolymers of methylhydrogensiloxane and trimethylsiloxane units, copolymers from methylhydrogensiloxane, diphenylsiloxane and trimethylsiloxane units, copolymers of methylhydrogensiloxane, dimethylhydrogensiloxane and diphenylsiloxane units, copolymers of methylhydrogensiloxane, phenylmethylsiloxane, trimethylsiloxane and
  • the organopolysiloxanes (1) have an average viscosity of preferably 5 to 5000 mm 2 / s at 25 ° C, preferably 20 to 500 mm 2 / s at 25 ° C.
  • formula (V) should be understood such that r units - (SiR 2 O) - and s units - (SiRHO) - can be distributed in any desired manner, for example as a block or randomly, in the organopolysiloxane molecule.
  • organopolysiloxanes (1) also apply in their entirety to organopolysiloxanes (2).
  • the organopolysiloxanes (2) have an average viscosity of preferably 50 to 5000 mm 2 / s at 25 ° C, preferably 50 to 500 mm 2 / s at 25 ° C.
  • the ratio of the viscosities of organopolysiloxanes (2) to organopolysiloxanes (1) is preferably at least 2.0, preferably at least 3.0, particularly preferably at least 5.0.
  • the viscosity ratio of organopolysiloxanes (2) to organopolysiloxanes (1) is at most 1000, preferably at most 100.
  • radicals R are alkyl radicals, such as the methyl, ethyl, n-propyl, iso-propyl, 1-n-butyl, 2-n-butyl, isobutyl, tert-butyl, n-pentyl, iso-pentyl, neo-pentyl, tert-pentyl, hexyl, such as the n-hexyl, heptyl, such as the n-heptyl, octyl, such as the n-octyl and iso-octyl, such as 2,2,4-trimethylpentyl radical, nonyl radicals such as the n-nonyl radical, decyl radicals such as the n-decyl radical, dodecyl radicals such as the n-dodecyl radical, and octadecyl radicals such as the n-octa
  • R is a methyl radical.
  • at least 99 mol%, particularly preferably 100 mol% of all R radicals are methyl radicals.
  • R 1 examples of hydrocarbon radicals R 1 are alkyl radicals, such as the methyl, ethyl, n-propyl, iso-propyl, 1-n-butyl, 2-n-butyl, isobutyl, tert-butyl , n-pentyl, iso-pentyl, neo-pentyl, tert-pentyl, hexyl, such as n-hexyl and iso-hexyl.
  • R 1 is a hydrogen atom.
  • polyether (3) at least two kinds of polyethers of the formulas (Ia) to (Ic) are used.
  • polyethers of different polarity are always used together. While (Ia) and (Ic) are homopolymers, (Ib) is a copolymer whose molar proportion of ethyleneoxy (EO) units is preferably in the range of about 1 to about 99 mol%, preferably in the range from about 4 to 80 mol% and more preferably in the range of about 10 to 65 mol%, the remainder being propyleneoxy units (PO units).
  • EO ethyleneoxy
  • the defoamer formulations preferably use silicone polyethers (B) which are prepared by reacting a mixture of polyethers of the formulas (Ib) and (Ic) with organopolysiloxanes (1).
  • the proportion of ethyleneoxy units of the polyethers of the formulas (Ib) and (Ic), based on the total number of alkyleneoxy units used, is preferably at most 50 mol%, preferably at most 40 mol% and particularly preferably at most 30 mol%. A particularly preferred range is from 10 to 30 mol%.
  • a particular advantage of the preparation method for the silicone polyethers (B) according to the invention is the possibility of precise and complete adjustment of their polarity, that is to say the ratio of organosiloxy, ethyleneoxy and propyleneoxy constituents in which the polyethers of the formulas (Ia), (Ib) and (Ic) cover a wide range of different products with only a few raw materials.
  • a 1 is in formulas (Ia), (Ib) and (Ic), and allyl polyethers are preferably used.
  • the same catalysts can be used in the inventive method, which could also be used to promote the attachment of Si-bonded hydrogen to aliphatic double bond.
  • the catalysts are preferably a metal from the group of platinum metals or a compound or a complex from the group of platinum metals.
  • platinum halides eg PtCl 4 , H 2 PtCl 6 * 6H 2 O, Na 2 PtCl 4 * 4H 2 O
  • platinum-olefin complexes platinum-alcohol complexes
  • platinum alkoxide Complexes platinum-ether complexes
  • platinum-aldehyde complexes platinum-ketone complexes, including reaction products of H 2 PtCl 6 * 6H 2 O and cyclohexanone
  • platinum-vinyl-siloxane complexes such as platinum-1,3-divinyl 1,1,3,3-tetramethyldisiloxane complexes with or without detectable inorganic halogenated content
  • bis (gamma-picoline) platinum dichloride trimethylene dipyridine platinum dichloride
  • the catalyst (4) is preferably used in the process according to the invention in amounts of from 1 to 50 ppm by weight (parts by weight per million parts by weight), preferably in amounts of from 5 to 20 ppm by weight, calculated in each case as elemental platinum and based on the total weight the components used (1), (2) and (3) used.
  • the catalyst (4) is added to polyether (3) before the addition of the organopolysiloxanes (1) and (2).
  • a portion of the amount of the catalyst is initially charged in the first step and in the second step, the remaining amount of the catalyst is added when operating in two steps.
  • the inventive method is preferably at a temperature of 60 to 120 ° C, preferably 80 to 120 ° C. carried out.
  • the process according to the invention is carried out at the pressure of the surrounding atmosphere, ie at about 1020 hPa, but it can also be carried out at higher or lower pressures.
  • Solvents may be included in the process of the invention. Examples of solvents are toluene, xylene, isopropanol, n-butanol. If solvents are used, they are preferably used in amounts of 5 to 20 wt .-% based on the reaction mixture. The concomitant use of solvent is not preferred.
  • formula (VIII) should be understood to mean that m units - (SiR 2 O) - and n units - (SiRAO) - in in any way, for example as a block or randomly, may be distributed in the organopolysiloxane molecule.
  • silicone polyether (B) there are preferably obtained those containing two different polyether groups A of the general formulas (VIIb) and (VIIc), the proportion of ethyleneoxy units in the polyether groups of the formulas (VIIb) and (VIIc) based on the total number of Alkyleneoxy, preferably at most 50 mol%, preferably at most 40 mol% and particularly preferably at most 30 mol%.
  • the silicone polyethers obtained by the process according to the invention have a viscosity of preferably 50 to 100,000 mPa.s at 25 ° C., preferably 100 to 20,000 mPa.s at 25 ° C.
  • the in situ hydrophobization of the silica (aa) can be carried out by heating the polyorganosiloxane dispersed in the polyorganosiloxane (ab) for several hours at temperatures of 100 to 200 ° C.
  • the reaction may be assisted by the addition of catalysts such as KOH and water repellents such as short chain OH-terminated polydimethylsiloxanes, silanes, silazanes or silicone resins.
  • catalysts such as KOH
  • water repellents such as short chain OH-terminated polydimethylsiloxanes, silanes, silazanes or silicone resins.
  • radicals R 8 in the general formula (II) are unsubstituted, branched or unbranched alkyl radicals, such as methyl, ethyl, propyl, isopropyl, hexyl, 2-ethylhexyl, octyl, or dodecyl radicals; substituted alkyl radicals such as trifluoropropyl, cyanoethyl, glycidoxypropyl, polyalkylene glycolpropyl, aminopropyl or aminoethylaminopropyl radicals; unsaturated radicals, such as vinyl, methacryloxypropyl or allyl radicals; aromatic radicals, such as phenyl, tolyl, xylyl, naphthyl, anthracyl or benzyl radicals.
  • Particularly preferred radicals R 8 are the methyl or phenyl radical, it being particularly preferred if more than 80 mol% of the radicals R 8 are methyl radical
  • radicals R 9 in the general formula (II) are unsubstituted, branched or unbranched alkyl radicals, such as methyl, ethyl, propyl, isopropyl, hexyl, 2-ethylhexyl, octyl, or dodecyl radicals; substituted alkyl radicals such as trifluoropropyl, cyanoethyl, glycidoxypropyl, polyalkylene glycolpropyl, aminopropyl or aminoethylaminopropyl radicals; unsaturated radicals, such as vinyl, methacryloxypropyl or allyl radicals; aromatic radicals, such as phenyl, tolyl, xylyl, naphthyl, anthracyl or benzyl radicals.
  • alkyl radicals such as methyl, ethyl, propyl, isopropyl, hexyl, 2-ethylhexy
  • Examples of compounds of the formula (IX) are polydimethylsiloxanes with viscosities of 100 to 1,000,000 mPa ⁇ s at 25 ° C. These polydimethylsiloxanes may, for. B. be branched by the incorporation of CH 3 SiO 3/2 - or SiO 4/2 units. These branched or cross-linked siloxanes then have viscoelastic properties.
  • Such branched viscoelastic polyorganosiloxanes can be obtained, for example, by reacting the dimethyldichlorosilane hydrolysis product or hydroxy-terminated polydimethylsiloxanes with a trimethylsilyl-terminated polydimethylsiloxane and a compound selected from a silane having at least three hydrolyzable groups such as tetraethoxysilane, methyltrimethoxysilane or methyltriacetoxysilane, or a silicone resin which substantially from (CH 3 ) 3 SiO 1/2 and SiO 2 units in the ratio of 2 to 1 to 1 to 2, in the presence of a catalyst.
  • Another variant for preparing branched viscoelastic polyorganosiloxanes is the reaction of an organosiloxane X 1 with statistically distributed, on average, less than 2 functional groups per molecule with an organosiloxane X 2 with randomly distributed, an average of more than 2 functional groups per molecule, with only one type of functional group being present per siloxane X 1 or X 2 , in the presence of a hydrosilylation-promoting catalyst, for example platinum or platinum compounds.
  • a hydrosilylation-promoting catalyst for example platinum or platinum compounds.
  • the siloxane-based antifoaming agent may contain 0.1 to 10% by weight, preferably 0.5 to 5% by weight, of at least one polyorganosiloxane (ab ') of the general formula (IX) in which R 8 is a methyl radical and R 9 is a linear and / or branched hydrocarbon radical having at least 6 carbon atoms, d has a value of 0.005 to 0.5 and the sum (d + e) assumes a value of 1.9 to 2.1.
  • Such products are accessible, for example, by alkaline-catalyzed condensation of silanol-terminated polydimethylsiloxanes having a viscosity of 50 to 50,000 mPa.s at 25 ° C.
  • aliphatic alcohols having more than 6 carbon atoms such as isotridecyl alcohol, n-octanol, stearyl alcohol, 4-ethylhexadecanol or eicosanol.
  • antifoam formulations it is possible to include further known additives or auxiliaries customary in antifoam formulations, for example further fillers, such as aluminum oxide, metal soaps, hydrophobized quartz flour or finely divided hydrophobic polyurethanes.
  • further fillers such as aluminum oxide, metal soaps, hydrophobized quartz flour or finely divided hydrophobic polyurethanes.
  • defoamer oils substances such as mineral oils, paraffin oils, fatty acid esters, fatty alcohols, polyoxyalkylenes such as Polyproypenglykole or ethylene oxide-propylene oxide copolymers, esters and ethers of polyoxyalkylenes, and waxes in amounts of 1 to 99 wt .-%, based on the total weight of the formulation is possible.
  • compounds known as thickeners such as polyacrylic acid, polyacrylates, cellulose ethers, such as carboxymethylcellulose and hydroxyethylcellulose, natural gums, such as xanthan gum and polyurethan
  • the preparation of the defoamer formulation according to the invention is carried out by known processes, for example using high shear forces in colloid mills or rotor-stator homogenizers.
  • the mixing process can be carried out at reduced pressure in order to prevent the mixing in of air which is contained in highly dispersed fillers.
  • defoamer formulations according to the invention in oil-in-water emulsions (O / W emulsions) is preferred.
  • the particular silicone polyethers used in the antifoam formulations according to the invention have surfactant properties and are therefore also suitable as emulsifiers for the formation of oil-in-water emulsions starting from antifoams based on siloxanes.
  • the defoamer formulations, when used as emulsions may also be supplemented with additional organic emulsifiers which may form O / W emulsions based on siloxanes.
  • the silicone polyethers (B) may be emulsified together with the antifoaming agent (A), or the silicone polyethers (B) may also be added to the antifoam emulsion directly or in the form of an emulsion after the preparation of an emulsion of the antifoaming agent (A) To improve the effect.
  • the emulsifiers required to prepare the emulsions can be anionic, cationic or nonionic and are known to those skilled in the preparation of stable silicone emulsions.
  • Emulsifier mixtures are preferably used, it being necessary to contain at least one nonionic emulsifier, such as, for example, sorbitan fatty acid esters, ethoxylated sorbitan fatty acid esters, ethoxylated fatty acids, ethoxylated linear or branched alcohols having 10 to 20 carbon atoms and / or glycerol esters.
  • silicone emulsions are known. Usually, the preparation is carried out by simply stirring all the components and then homogenizing with rotor-stator homogenizers, colloid mills or high-pressure homogenizers.
  • the antifoam formulations according to the invention can be used wherever there is a disturbing foam formation during processes which is to be reduced or completely eliminated. This is z.
  • the use in detergents and cleaners the control of foam in wastewater systems, in textile dyeing processes, in natural gas scrubbing, in dispersions and in hydrocarbons.
  • the antifoam formulations according to the invention are outstandingly suitable for defoaming aqueous media obtained during pulp production.
  • polymer 2 a commercial unbranched polyether-polysiloxane copolymer having a viscosity of 1100 mPa.s at 25 ° C. and a cloud point of> 25 ° C. was used.
  • the chain length of the pendant polyether-polysiloxane copolymer is about 50 Si units
  • the ratio of dimethylsiloxy (D) to methylpolyethersiloxy (D ') units is about 7: 1
  • the mole% share of the EO content is 74% and that of PO is 26%.
  • inventive defoamer formulations C11, C12, C13 and defoamer formulations V11, V12 and V13 and V14, V15 and V16 were prepared by simply mixing 90 parts of the silicone defoamer listed in the table and 10 parts of the silicone polyether indicated in the table laboratory dissolver.
  • a mixture of 40 parts of this defoamer formulation and 60 parts of a mixture of aliphatic hydrocarbons having a viscosity of 3 mm 2 / s and a flash point> 100 ° C was prepared with a laboratory dissolver at 1000 min -1 .
  • the results of the effectiveness test are summarized in the table.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Toxicology (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Silicon Polymers (AREA)
  • Degasification And Air Bubble Elimination (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Paper (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
EP10169956A 2009-07-27 2010-07-19 Formules d'agents anti-moussants Revoked EP2289977B1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102009028041A DE102009028041A1 (de) 2009-07-27 2009-07-27 Entschäumerformulierungen

Publications (2)

Publication Number Publication Date
EP2289977A1 true EP2289977A1 (fr) 2011-03-02
EP2289977B1 EP2289977B1 (fr) 2012-02-01

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ID=43015803

Family Applications (1)

Application Number Title Priority Date Filing Date
EP10169956A Revoked EP2289977B1 (fr) 2009-07-27 2010-07-19 Formules d'agents anti-moussants

Country Status (7)

Country Link
US (1) US8222303B2 (fr)
EP (1) EP2289977B1 (fr)
JP (1) JP2011025239A (fr)
KR (1) KR101230455B1 (fr)
CN (1) CN101966403A (fr)
AT (1) ATE543856T1 (fr)
DE (1) DE102009028041A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3954740A1 (fr) * 2020-08-14 2022-02-16 Evonik Operations GmbH Composition antimousse basée sur les polysiloxanes organo-fonctionnels modifiés

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DE102007047211A1 (de) * 2007-10-02 2009-04-09 Wacker Chemie Ag Entschäumerzusammensetzungen
DE102008000525A1 (de) * 2008-03-05 2009-09-10 Wacker Chemie Ag Verfahren zur Herstellung von Siliconpolyethern
US8846585B2 (en) * 2010-09-17 2014-09-30 Clearwater International, Llc Defoamer formulation and methods for making and using same
GB201102750D0 (en) 2011-02-16 2011-03-30 Dow Corning Foam control composition
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CN102286203A (zh) * 2011-06-29 2011-12-21 南京四新科技应用研究所有限公司 一种提高有机硅乳液稳定性的方法
US8735524B2 (en) * 2011-09-09 2014-05-27 Air Products And Chemicals, Inc. Silicone containing compositions and uses thereof
CA2863076C (fr) * 2012-02-01 2020-09-08 Momentive Performance Materials Inc. Copolymeres de siloxane-polyether
RU2615144C2 (ru) 2012-02-16 2017-04-04 Дау Корнинг Корпорейшн Гранулированное вещество для контроля пенообразования для цикла полоскания с использованием силоксанового воска
GB201314284D0 (en) 2013-08-09 2013-09-25 Dow Corning Cosmetic compositions containing silicones
MX374935B (es) 2013-08-13 2025-03-06 Dow Corning Metodo para formar un granulo antiespuma.
KR102391671B1 (ko) * 2014-02-04 2022-04-29 솔레니스 테크놀러지스, 엘.피. 펄프의 브라운스톡 세척을 위한 소포제의 현장 에멀젼화
CN103923323B (zh) * 2014-04-21 2017-02-08 西安三业精细化工有限责任公司 一种三元共聚体消泡剂的制备方法
US20160066567A1 (en) * 2014-09-09 2016-03-10 Wacker Chemical Corporation Stable defoamers for high electrolyte agricultural formulations
US9815003B2 (en) 2015-09-28 2017-11-14 Wacker Chemical Corporation Silicone defoamer compositions
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JP6862539B2 (ja) * 2017-06-06 2021-04-21 ワッカー ケミー アクチエンゲゼルシャフトＷａｃｋｅｒ Ｃｈｅｍｉｅ ＡＧ オルガノポリシロキサンを含む消泡配合物
CN108726913B (zh) * 2018-05-28 2021-04-27 天津中油渤星工程科技有限公司 一种硅醚复合消泡剂及其制备方法和应用
CN108997815B (zh) * 2018-09-04 2021-05-14 南京瑞思化学技术有限公司 一种聚醚组合物
EP3887016B1 (fr) * 2018-11-28 2022-06-15 Wacker Chemie AG Formulations antimousses contenant des organopolysiloxanes
CN110465119A (zh) * 2019-08-28 2019-11-19 启东曦瑞新材料科技有限公司 一种矿物油消泡剂的制备方法
CN111534360A (zh) * 2020-03-05 2020-08-14 郑州大学 一种水性防锈消泡剂及其制备方法
US12134745B2 (en) * 2020-12-28 2024-11-05 Dow Toray Co., Ltd. Oil compound for silicone-based defoaming agents, method for producing same, and defoaming agent containing oil compound for silicone-based defoaming agents
CN116457393B (zh) 2020-12-28 2025-09-30 陶氏东丽株式会社 有机硅系消泡剂组合物
CN114316609B (zh) * 2021-09-03 2023-04-25 南京瑞思化学技术有限公司 一种硅醚组合物的制备方法
WO2025010126A1 (fr) 2023-07-06 2025-01-09 Dow Silicones Corporation Copolymère silicone-polyéther destiné à être utilisé dans des formulations de régulation de mousse
WO2025160735A1 (fr) 2024-01-30 2025-08-07 Wacker Chemie Ag Composition

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US12053721B2 (en) 2020-08-14 2024-08-06 Evonik Operations Gmbh Defoamer composition based on organofunctionally modified polysiloxanes

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KR101230455B1 (ko) 2013-02-06
EP2289977B1 (fr) 2012-02-01
DE102009028041A1 (de) 2011-02-03
ATE543856T1 (de) 2012-02-15
JP2011025239A (ja) 2011-02-10
US20110021688A1 (en) 2011-01-27
KR20110011539A (ko) 2011-02-08
CN101966403A (zh) 2011-02-09

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